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Drilling Fluid:
Hole cleaning
Hole cleaning is one
of the basic functions of any drilling fluid. Cuttings generated by the
bit, plus any caving and/or sloughing, must be carried to the surface by
the mud.
Failure to achieve
effective hole cleaning can lead to serious problems, including stuck
pipe, excessive torque and drag, annular pack-off, lost circulation, high
mud costs and slow drilling rates. Cuttings transport is affected by
several interrelated mud and drilling parameters.
Removing cuttings
from below the drill bit is still a crucial function of a drilling fluid.
The circulatory fluid rising from the bottom of the well bore carries the
cuttings toward the surface.
Under the influence
of gravity, these cuttings tend to fall through the ascending fluid. This
is known as slip velocity.
The slip velocity
will depend upon the viscosity (thickness) and density of the fluid. The
thicker the fluid, the lower the slip velocities. The more dense the
fluid, the lower the slip velocity. For effective cuttings removal, the
fluid velocity must be high enough to overcome the slip velocity of the
cuttings.
This means that
fluid velocity can be lowered in a highly viscous (thick) or very dense
fluid and cuttings still effectively removed from the well
bore.
The density of a
fluid is determined by other factors and is not usually considered a
factor in hole cleaning; therefore we limit adjustment of hole cleaning
properties to viscosity and velocity adjustments to the drilling
fluid.
The viscosity
desired will depend upon the desired hydraulics and the size of the
cuttings contained in the fluid. The velocity will depend on several
factors -the pump (capacity, speed, efficiency), the drill pipe size and
the size of the bore hole.
The velocity of a
fluid will determine its flow characteristics, or flow
profile.
There are five
stages, or different profiles, for a drilling fluid: (1) no
flow, (2) plug flow, (3) transition, (4)
laminar, 95) turbulent.
The ideal velocity
is one that will achieve laminar (or streamline) flow because it provides
the maximum cuttings removal without eroding the well
bore.
On the other hand,
turbulent flow (resulting from too high a velocity or too low fluid
viscosity) not only requires more horsepower but can cause excessive hole
erosion and undesirable hole enlargement.
The proper
combination of velocity and viscosity is a must for the right hydraulics
and efficient hole cleaning. Cuttings will have a tendency to collect at
points of low fluid velocity in the well bore annulus.
These areas are
found in washouts and where the drill pipe rests against the wall of the
well bore. To that end, it is a good practice to rotate and work (raise
and lower ) the drill string while just circulating to clean the hole, as
this will help keep the cuttings in the main flow of the fluid and not
allow them to gather next to the wall or pipe.
Hole angle, annular
velocity and mud viscosity are considered to be the most important.
Cuttings and particles that must be circulated from the well have three
forces working on them:
(1) a downward force
due to gravity, (2) an upward force due to buoyancy from the
fluid and (3) a force parallel to the direction of the mud flow
due to mud flowing around the particle.
The hole-cleaning
process must counteract gravitational forces acting on cuttings to
minimize settling during both dynamic and static periods. Three basic
settling mechanisms can apply:
(1) free, (2)
hindered and (3) Boycott settling.
Free settling
occurs when a single particle falls through a fluid without interference
from other particles or container walls. The larger the difference between
the density of the cutting and the density of the liquid, the faster the
particle will settle.
The larger the particle is the faster
it settles and the lower the liquid’s viscosity, the faster the settling
rate. Hindered settling is more realistic settling mode for near-vertical
and near-horizontal intervals.
Hindered settling
occurs when fluid displaced by falling particles creates upward forces on
adjacent particles, thereby slowing down their settling
rate.
The net results is
still an overall downward movement, but the settling rate is always less
(hindered), thus the name. Boycott settling is an accelerated settling
pattern that can occur in inclined well bores.
Boycott settling is
the consequence of rapid settling adjacent to the high and low sides of
inclined well bores. This causes a pressure imbalance which drives the
lighter, upper fluid upwards and any cutting beds on the low side
downwards.
At relatively low
flow rates, mud flows mainly along the high side and accelerates or
enhances the Boycott effect. High flow rates and pipe rotation can disrupt
the pattern and improve hole cleaning.
If not properly
supported, cuttings can accumulate at the bottom of the hole or on the low
side of inclined intervals. "Plugs" and stuck pipe can be caused by
dragging bottom hole tools up through pre-existing beds.
Cuttings
accumulations can be difficult to erode or re-suspend, so mud properties
and drilling practices which minimize their formation should be
emphasized.
Cuttings transport
efficiency is largely a function of annular velocity and the annular
velocity profile. Increasing annular velocity will always improve hole
cleaning, though it still must work with other hole parameters. In fully
concentric annulus, flow is evenly distributed around the drill
string.
Thus there is an
equal distribution of fluid energy for cuttings transport. However, the
drill string tends to lay on the low side of the hole in inclined
sections, shifting or skewing the velocity profile, the results of which
is not conducive to cuttings transport.
Cuttings accumulate
on the bottom of the hole adjacent to the drill pipe where the mud flow is
minimal. In this situation, pipe rotation is critical to achieve effective
hole cleaning. However, there are times when drilling a directional hole
that pipe rotation will not be possible.
All is not lost at
this point since we can offset the detrimental effects of not rotating
with different mud types and changing certain mud properties.
Generally speaking,
different drilling fluid types provide similar cuttings transport if their
down hole properties are similar.
Properties of
particular interest to hole cleaning include mud weight, viscosity and gel
strengths. Mud weight helps buoy cuttings and slow their settling rate but
it is really not used to improve hole cleaning. Instead, mud weights
should be adjusted based only on pore pressure, fracture gradient and
well-bore stability requirements.
Mud viscosities
helps determine carrying capacity. Yield points historically has been used
as the key parameter which was though to affect hole
cleaning.
More recently,
evidence concludes that Fann 6 and 3 RPM values are better indicators of
carrying capacity. These values are more representative of the Low Shear
Rate Viscosity (LSRV) which affects hole cleaning in marginal situations.
One common rule of thumb is to maintain the 3 RPM value so that it is
greater than the hole size (expressed in inches) in high angle
wells.
Gel strengths
provide suspension under both static and low shear rate conditions. The
ideal situation is for the fluid to have high, fragile gels that develop
quickly and are easily broken. Excessive high, progressive gels, on the
other hand, should be avoided as they cause high transient pressures that
cause a number of serious drilling problems.
Listed below are
practical hole-cleaning guidelines aimed at field use on directional
bores.
Use hole-cleaning
techniques to minimize cuttings-bed formation and subsequent slumping
which can occur in 30-60 degree hole sections.
Utilize
elevated-viscosity fluids from the start because cuttings beds are easy
to deposit but difficult to remove.
Maintain LSRV
between 1.0 and 1.2 times the hole diameter when in laminar flow. This
requirement will be easier to accomplish if the fluid is treated with a
super's or high vis. This product is a bio-polymer that elevates the
LSRV in fluids.
Treat mud to
obtain elevated, flat gels for suspension during static and low flow
rate periods. Consider using the mud system that will give you excellent
LSRV values and superior suspension abilities. The system uses an
untreated bentonite and a mixed metal hydroxide additive.
Schedule periodic
wiper trips and pipe rotation intervals for situations where sliding
operations are extensive.
Rotate pipe at
speeds above about 50 RPM if possible to prevent bed formations and to
help remove pre-existing beds.
Expect little help
from viscous sweeps, unless they are accompanied by high flow rates and
pipe rotation
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